WO2019178459A1 - Turbine à séparation supersonique - Google Patents

Turbine à séparation supersonique Download PDF

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Publication number
WO2019178459A1
WO2019178459A1 PCT/US2019/022436 US2019022436W WO2019178459A1 WO 2019178459 A1 WO2019178459 A1 WO 2019178459A1 US 2019022436 W US2019022436 W US 2019022436W WO 2019178459 A1 WO2019178459 A1 WO 2019178459A1
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WO
WIPO (PCT)
Prior art keywords
vapor stream
turbine
stream
processing unit
supersonic
Prior art date
Application number
PCT/US2019/022436
Other languages
English (en)
Inventor
Stanley Joseph Frey
Michael VAN DE COTTE
Original Assignee
Uop Llc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Uop Llc filed Critical Uop Llc
Priority to EP19767007.8A priority Critical patent/EP3765171B1/fr
Priority to JP2020547140A priority patent/JP7110376B2/ja
Publication of WO2019178459A1 publication Critical patent/WO2019178459A1/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
    • F01D15/10—Adaptations for driving, or combinations with, electric generators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
    • F01D25/32—Collecting of condensation water; Drainage ; Removing solid particles
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2220/00—Application
    • F05D2220/30—Application in turbines
    • F05D2220/31—Application in turbines in steam turbines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2220/00—Application
    • F05D2220/60—Application making use of surplus or waste energy
    • F05D2220/62—Application making use of surplus or waste energy with energy recovery turbines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2220/00—Application
    • F05D2220/70—Application in combination with
    • F05D2220/76—Application in combination with an electrical generator
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2260/00—Function
    • F05D2260/14—Preswirling
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26—Steam-separating arrangements
    • F22B37/32—Steam-separating arrangements using centrifugal force

Definitions

  • This invention relates generally to a turbine used in vapor stream in a chemical processing or refining plant, and more particularly to a turbine used with a vapor stream that is at or near its dew point.
  • Control valves are used to control the flow, upstream or downstream pressure, temperatures, or levels, etc.
  • mechanical energy is dissipated. Since the energy is dissipated, without recovery, the energy is lost.
  • the turbine could potentially be problematic. Specifically, in a vapor stream at or near its dew point, when the vapor stream passes through the turbine and its pressure is reduced, the resultant vapor stream will partially condense forming a two-phase stream as a result of the cooling of expansion of the vapor. While there are currently turbines that are designed to accommodate the two-phase stream, such turbines are complicated in design and difficult to predict in operation.
  • the present invention attempts to overcome one or more shortcomings discussed above.
  • upstream of the turbine is a supersonic separator which separates out the heavier components before the vapor stream is passed to the turbine.
  • the supersonic separator imparts a swirl at sonic or supersonic velocity to the vapor which condenses some of the heavier compounds into droplets.
  • the droplets are separated from the remaining vapor phase components which are then passed to the turbine for a pressure reduction while generating electricity.
  • the turbine is able to provide information about the amount of energy removed. This information may be utilized to in determining adjustments for various processing conditions which reduce the amount of energy added to the process. This permits the processor to more efficiently operate the processing unit without reducing the throughput of the processing unit.
  • the present invention may be characterized, in at least one aspect, as providing a process for recovering power from a vapor stream with a turbine by: condensing a portion of the vapor stream in a supersonic separation device, the separation supersonic device configured to impart a swirl at or above a sonic velocity on the vapor stream passing therethrough; separating the condensed portion from the vapor stream with the supersonic separation device to provide a superheated vapor stream; and, recovering power from the superheated vapor stream in a turbine, the turbine comprising a turbine wheel configured to transmit rotational movement to an electrical generator.
  • the present invention may be generally characterized as providing a process for recovering power from a vapor stream with a turbine by: passing a vapor stream to a supersonic separation device, the supersonic separation device configured to impart a swirl at or above a sonic velocity on the vapor stream passing therethrough; separating a condensed portion of the vapor stream with the supersonic separation device to provide a superheated vapor stream; passing the superheated vapor stream to a turbine, the turbine comprising a turbine wheel configured to transmit rotational movement to an electrical generator; rotating the turbine wheel with the superheated vapor stream; and, generating electricity with the electrical generator.
  • the present invention may be characterized as providing an apparatus for generating electricity which includes: a body with an inlet configured to receive a vapor stream, a first outlet for a superheated vapor stream and, a second outlet for a liquid stream; a baffle disposed within the body and configured to impart a swirl at or above sonic velocity to the vapor stream; an internal cavity in the body between the inlet, the first outlet, and the second outlet; and, a turbine wheel configured to transmit rotational movement from the superheated vapor stream to an electrical generator, the turbine wheel disposed between the outlet and the internal cavity.
  • Figure 1 depicts a partial cutaway schematic view of a device according to the present invention.
  • Figure 2 depicts a hydroprocessing unit according to one or more embodiments of the present invention.
  • the present invention provides a supersonic separating device upstream of a turbine.
  • the supersonic separating device condenses a portion of a vapor stream that is at or near its due point.
  • the remaining vapor portion, a superheated stream as a result of the heavier compounds being removed, is passed through the turbine, allowing the pressure to be reduced.
  • the turbine generates electricity from this energy dissipation which is recovered or used elsewhere in the processing unit.
  • the reduced pressure vapor stream is less likely to be a two-phase system and can be used as desired in the process unit.
  • FIG. 1 An exemplary device 10 according to the present invention is shown in Figure 1.
  • the device 10 is used for generating electricity and a vapor stream with a lower pressure.
  • the device 10 includes a supersonic separator 12 and a turbine 14. It is contemplated that the supersonic separator 12 and the turbine 14 are integrally formed as a single unit, i.e., the two are contained within a single body 15 (or housing) and are not connected to each other with any external conduits. This is merely a preferred configuration, and it is contemplated that the advantages and benefits of the present invention are achieved with the supersonic separator 12 and the turbine 14 being discrete components as opposed to a single unit.
  • the particular configuration of the supersonic separator 12 is not necessarily important for the practicing of the present invention.
  • Exemplary supersonic separators 12 are disclosed in U.S. Pat. Nos. 6,962, 199, 7,261,766, 7,318,849, 7,494,535, 8,257,458, 8,398,734, 7,909,912, 8,475,555, 8,657,930, and 9,034,082, all of which are incorporated herein by reference.
  • the supersonic separator 12 comprises an inlet 16 configured to receive a vapor stream 18, a first outlet 19 for a superheated vapor stream 20 and, a second outlet 22 for a liquid stream 24.
  • the vapor stream 18 is at or near its dew point.
  • the vapor stream 18 could be within 10 °C of a dew point of the vapor stream 18, within 5 °C of a dew point of the vapor stream 18, within 1 °C of a dew point of the vapor stream 18, or greater than the dew point of the vapor stream 18 but less than 1 °C from the dew point of the vapor stream 18.
  • the vapor stream 18 includes hydrogen gas and light hydrocarbons, hydrogen sulfide, ammonia, and water. By light hydrocarbons it is meant that the hydrocarbons in the vapor stream 18 comprise between one and six carbon atoms.
  • the supersonic separator 12 Within the supersonic separator 12 one or more baffles 26 impart a swirl at or above sonic velocity to the vapor stream 18. Downstream of the baffle(s) 26 the supersonic separator 12 includes an internal cavity 28. As is known in the art, within the internal cavity 28, the swirling vapor stream causes the larger molecules and compounds within the swirling vapor stream to condense together for form droplets. The droplets separate from the vapor and are recovered as the liquid stream 24 from the supersonic separator 12 via the second outlet 22. [00022] Downstream of the internal cavity 28, the vapor is a superheated vapor stream 20 that is passed to the turbine 14. The superheated vapor stream 20 has the same, or approximately the same temperature as the vapor stream 18.
  • the superheated vapor stream 20 may or may not have a different chemical composition than the vapor stream 18. It is contemplated that the superheated vapor stream 20 has at least 2 °C more superheat the vapor stream 18.
  • the superheated vapor stream 20 is passed to the turbine 14 for a pressure reduction and to generate electricity.
  • the turbine 14 includes a turbine wheel 30 with blades 32 configured to transfer, or transmit, rotational movement, created by the flow of a fluid stream passing the turbine wheel 30, to an electrical generator 34.
  • the electrical generator 34 generally includes a first winding 36, in communication with the turbine wheel 30 and a second winding 38 surrounding the first winding 36 and stationary with respect to the first winding 36.
  • the rotation of the first winding 36 creates an electrical current in the second winding 38.
  • the turbine 14 may include a processor 40 configured to measure an amount of electricity generated by the turbine 14 and a transmitter 42 configured to transmit information associated with the amount of electricity generated by the turbine 14 to a computer 44 at a control center 46 for the processing unit (discussed in more detail below).
  • the superheated vapor stream 20 passing therethrough will rotate the turbine wheel 30 and, as is known, generate electricity via the electrical generator 34.
  • the pressure of the superheated vapor stream 20 is reduced to provide a low pressure vapor stream 48 having a pressure that is less than the superheated vapor stream 20 (and the vapor stream 18).
  • the low pressure vapor stream 48 is less likely to be two-phase— even though the vapor stream 18 was at or near its dew point.
  • the present invention provides for the conversion of some of the energy removed via the pressure reductions to electricity.
  • the process according to the present invention comprises directing a portion of a gaseous process stream through one or more variable-resistance turbines to control the flowrate of the gas process stream and, optionally, generate electric power therefrom; controlling a pressure and temperature of the gaseous process stream so that the gas exiting the power-recovery turbine remains in the gas phase; and measuring the flowrate or controlling the flowrate or both using a variable nozzle turbine, inlet variable guide vanes, or direct coupled variable electric load, to name a few, to vary the resistance to flow through the turbine.
  • the resistance to rotation of the variable- resistance turbine can be varied by an external variable load electric circuit which is in a magnetic field from a magnet(s) that is rotating on the turbine.
  • An algorithm in the device can also calculate the actual flow through the device by measuring the turbine RPMs and the load on the circuit.
  • the resistance to rotation flow can also be varied by variable position inlet guide vanes.
  • the power will be generated via power-recovery turbines with variable resistance to flow made possible by either guide vanes or variable load on the electrical power generation circuit.
  • An algorithm to calculate actual flow using the guide vanes position, power output and RPMs can be used.
  • a slow responding application is contemplated to have a response time to reach half way (i.e., 50% of a difference) between a new (or target) steady state condition (e.g., temperature, pressure, flow rate) from an original (or starting) steady state condition when the new (or target) condition differs from the original (or stating) condition of at least 10%, is of at least one second, or even greater, for example, ten seconds, at least one minute, at least ten minutes, or an hour or more, for half of the change to completed.
  • a new (or target) steady state condition e.g., temperature, pressure, flow rate
  • FIG 2 another embodiment of the present invention is shown in relation to a hydroprocessing unit 300.
  • hydrogen stream 305 is compressed in compressor 310.
  • the compressed hydrogen stream 315 is split into first and second portions, hydrogen streams 320 and 325.
  • First hydrogen stream 320 is mixed with the hydrocarbon feed stream 330 and sent through heat exchanger 335 to raise the temperature.
  • the partially heated feed stream 340 is sent to fired heater 345 to raise the temperature of the feed stream 350 exiting the fired heater 345 to the desired inlet temperature for the hydroprocessing reaction zone 355.
  • Second hydrogen stream 325 is divided into four hydrogen quench streams 390, 395, 400, 405.
  • Each of the hydrogen quench streams 390, 395, 400, 405 has a turbine 410, 415, 420, 425 configured to generate power and control the flow of hydrogen entering the hydroprocessing bed as well as a control valve 430, 435, 440, 445 to control the flow of hydrogen entering the hydroprocessing bed.
  • the turbines 410, 415, 420, 425 each include a supersonic separator 41 1, 416, 421, 426 and thus may have the configuration shown in FIGURE 1, discussed above.
  • Hydrogen quench streams 390, 395, 400, 405 can be directed through either the turbine 410, 415, 420, 425, the control valve 430, 435, 440, 445, or both.
  • a first fraction of the second hydrogen stream 325 can be directed to the first supersonic separator 411 and turbine 410, and a second fraction can be directed to the control valve 430.
  • the first fraction can vary from 0% to 100% and the second fraction can vary from 100% to 0%.
  • the flow of the hydrogen quench streams 390, 395, 400, 405 can be controlled by the turbines 410, 415, 420, 425, the control valves 430, 435, 440, 445, or both, allowing excellent process flexibility in systems including both.
  • hydroprocessing reaction zone 355 has five hydroprocessing beds 360, 365, 370, 375, and 380.
  • Feed stream 350 which contains hydrogen and hydrocarbon feed to be hydroprocessed, enters the first hydroprocessing bed 360 where it undergoes hydroprocessing.
  • the effluent from the first hydroprocessing bed 360 is mixed with first hydrogen quench stream 390 to form first quenched hydroprocessed stream 450.
  • the first quenched hydroprocessed stream 450 is sent to the second hydroprocessing bed 365 where it undergoes further hydroprocessing.
  • the effluent from the second hydroprocessing bed 365 is mixed with second hydrogen quench stream 395 to form second quenched hydroprocessed stream 455.
  • the second quenched hydroprocessed stream 455 is sent to the third hydroprocessing bed 370 where it undergoes further hydroprocessing.
  • the effluent from the third hydroprocessing bed 370 is mixed with third hydrogen quench stream 400 to form third quenched hydroprocessed stream 460.
  • the third quenched hydroprocessed stream 460 is sent to the fourth hydroprocessing bed 375 where it undergoes further hydroprocessing.
  • the effluent from the fourth hydroprocessing bed 375 is mixed with fourth hydrogen quench stream 405 to form fourth quenched hydroprocessed stream 465.
  • the fourth quenched hydroprocessed stream 465 is sent to the fifth hydroprocessing bed 380 where it undergoes further hydroprocessing.
  • the effluent 470 from the fifth hydroprocessing bed 380 can be sent to various processing zones, as described above.
  • the effluent 470 typically is heat exchanged with the feed, passed to a water wash to extract and dissolve salts, air or water cooled with a condensing heat exchange, and subjected to a vapor liquid separation to provide a recycle gas and liquid— which is passed to subsequent stripping and distillative fractionation.
  • the recycle gas stream would be amine treated to remove hydrogen sulfide, combined with make-up hydrogen before or after recompression in a recycle gas compressor and returned to the hydroprocessing reaction zone 355 via the combining with the reactor inlet hydrocarbon stream or as quench gas streams along the length of the reactor.
  • the chemical processing units used in the present processes utilize a process control system.
  • the process control system described in connection with the embodiments disclosed herein may be implemented or performed on the computer with a general purpose processor, a digital signal processor (DSP), an application specific integrated circuit (ASIC), a field programmable gate array (FPGA) or other programmable logic device, discrete gate or transistor logic, discrete hardware components, or any combination thereof designed to perform the functions described herein.
  • a general-purpose processor may be a microprocessor, or, the processor may be any conventional processor, controller, microcontroller, or state machine.
  • a processor may also be a combination of computing devices, e.g., a combination of a DSP and a microprocessor, two or more microprocessors, or any other combination of the foregoing.
  • a software module may reside in RAM memory, flash memory, ROM memory, EPROM memory, EEPROM memory, registers, hard disk, a removable disk, a CD-ROM, or any other form of storage medium known in the art.
  • An exemplary storage medium is in communication with the processor reading information from, and writing information to, the storage medium. This includes the storage medium being integral to or with the processor.
  • the processor and the storage medium may reside in an ASIC.
  • the ASIC may reside in a user terminal.
  • the processor and the storage medium may reside as discrete components in a user terminal.
  • processors and storage medium or memory are also typically in communication with hardware (e.g., ports, interfaces, antennas, amplifiers, signal processors, etc.) that allow for wired or wireless communication between different components, computers processors, or the like, such as between the input channel, a processor of the control logic, the output channels within the control system and the operator station in the control center.
  • hardware e.g., ports, interfaces, antennas, amplifiers, signal processors, etc.
  • the transmission of the data or information can be a wireless transmission (for example by Wi-Fi or Bluetooth) or a wired transmission (for example using an Ethernet RJ45 cable or an USB cable).
  • a wireless transceiver for example a Wi-Fi transceiver
  • the transmission can be performed automatically, at the request of the computers, in response to a request from a computer, or in other ways. Data can be pushed, pulled, fetched, etc., in any combination, or transmitted and received in any other manner.
  • the process control system receives information relative to an amount of electricity generated by the turbines 14, 410, 415, 420, 425. It is contemplated that the turbine 14, 410, 415, 420, 425 determines the amount of electricity it has generated, or alternatively, the process control system receiving the information determines the amount of electricity that has been generated. In either configuration, the amount of the electricity generated by the turbines 14, 410, 415, 420, 425 is displayed on at least one display screen 50 (for example in communication with the computer 44 in the control center 46).
  • the processing control system receives information associated with the amount of electricity generated by each of the turbines 14, 410, 415, 420, 425.
  • the processing control system determines a total power generated based upon the information associated with the each of the turbines 14, 410, 415, 420, 425and displays that the total power generated.
  • the total power generated may be displayed instead of or in conjunction with the display of the power generated by individual turbines 14, 410, 415, 420, 425.
  • the processes according to the present invention provide for the various processing conditions associated with the processing units to be adjusted into order to lower the energy added to the steam initially. It is contemplated that the process control system receives information associated with the throughput of the processing unit, and determines a target power generated value for the turbines 14, 410, 415, 420, 425, since the electricity represents energy that is typically added to the overall processing unit. The determination of the target power generated value may be done when the electricity is at or near a predetermined level.
  • the process control system will analyze one or more changes to the various processing conditions associated with the processing unit to lower the amount of energy recovered by the turbines 14, 410, 415, 420, 425.
  • the processing conditions are adjusted without adjusting the throughput of the processing unit. This allows for the processing unit to have the same output, but with a lower operating input.
  • the process control software may calculate and display the difference between the target power generated value and the total power generated on the at least one display screen 50.
  • the process control system receives information associated with the throughput of the processing unit, and determines a target electrical power generated value for the turbine(s) 14, 410, 415, 420, 425 since the electricity represents energy that is typically added to the overall processing unit.
  • the determination of the target electrical power generated value may be done when the electricity is at or near a predetermined level. In other words, if the amount of electricity produced meets or exceeds a predetermined level, the processing simulation system can determine one or more processing conditions to adjust and lower the amount of electricity generated until it reaches the target electrical power generated value.
  • the process simulation system will analyze one or more changes to the various processing conditions associated with the processing unit to lower the amount of energy recovered by the turbine 14, 410, 415, 420, 425.
  • the processing conditions are adjusted without adjusting the throughput of the processing unit. This allows for the processing unit to have the same throughput, but with a lower operating cost.
  • the process simulation software may calculate and display the difference between the target electrical power generated value and the total electrical power generated on the at least one display screen 50.
  • the process simulation software may determine that the total electrical power generated exceeds a predetermined level. Accordingly, the process simulation software determines the target electrical power generated value. Based upon other data and information received from other sensors and data collection devices typically associated with the processing unit, the process simulation software determines that the pressure provided by a compressor associated with the vapor stream can be lowered. While maintaining the throughput of the processing unit, an operating condition of the compressor is adjusted to provide a vapor stream 18 that still needs a pressure reduction in the turbine 14, 410, 415, 420, 425, but the difference between the two pressures is smaller. While this may lower the electricity generated by the turbine 14, 410, 415, 420, 425, the lower pressure for the compressor output requires less energy to achieve and provides a lower operating cost for the same throughput.
  • the processing units are provided with opportunities to lower the energy input associated with the overall processing unit and increase profits by utilizing more energy efficient processes.
  • a first embodiment of the invention is a process for recovering power from a vapor stream with a turbine, the process comprising condensing a portion of the vapor stream in a supersonic separation device, the supersonic separation device configured to impart a swirl at or above a sonic velocity on the vapor stream passing therethrough; separating the condensed portion from the vapor stream with the supersonic separation device to provide a superheated vapor stream; and, recovering power from the superheated vapor stream in a turbine, the turbine comprising a turbine wheel configured to transmit rotational movement to an electrical generator.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph, wherein the superheated vapor stream has at least 2 °C more superheat than the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph, wherein a temperature of the vapor stream is less than 10 °C above a dew point of the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph, wherein the temperature of the vapor stream is less than 5 °C above a dew point of the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph, wherein the vapor stream comprises hydrogen and light hydrocarbons.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph, wherein the condensed portion comprises the light hydrocarbons.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the first embodiment in this paragraph wherein the supersonic separation device and the turbine are integral with each other.
  • a second embodiment of the invention is a process for recovering power from a vapor stream with a turbine, the process comprising passing a vapor stream to a supersonic separation device, the supersonic separation device configured to impart a swirl at or above a sonic velocity on the vapor stream passing therethrough; separating a condensed portion of the vapor stream with the supersonic separation device to provide a superheated vapor stream; passing the superheated vapor stream to a turbine, the turbine comprising a turbine wheel configured to transmit rotational movement to an electrical generator; rotating the turbine wheel with the superheated vapor stream; and, generating electricity with the electrical generator.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the superheated vapor stream has at least 2 °C more superheat than the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein a temperature of the vapor stream is less than 10 °C above a dew point of the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the temperature of the vapor stream is less than 5 °C above a dew point of the vapor stream.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the vapor stream comprises hydrogen and light hydrocarbons.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the condensed portion comprises the light hydrocarbons.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph wherein the supersonic separation device and the turbine are integral with each other.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph further comprising receiving information from the turbine relative to an amount of electricity generated by the turbine; and, displaying the amount of electricity generated by the turbine on at least one display screen.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph further comprising receiving information associated from a plurality of turbines relative to an amount of information generated by each of the turbines; determining a total amount of electricity generated by the turbines; and, displaying the total amount of electricity generated on the at least one display screen.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the vapor stream is part of a processing unit, and the process further comprising receiving information associated with a throughput of the processing unit; and, determining a power generated target value based in part on the information associated with the throughput of the processing unit.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph further comprising maintaining the throughput of the processing unit while adjusting at least one process parameter of the processing unit based upon the power generated target value.
  • An embodiment of the invention is one, any or all of prior embodiments in this paragraph up through the second embodiment in this paragraph, wherein the processing unit comprises a plurality of turbines each configured to generate electricity, and wherein the process comprises determining a total power generated based upon the amount of electricity generated by each of the turbines; and, displaying the total power generated on the at least one display screen.
  • a third embodiment of the invention is an apparatus for generating electricity, the apparatus comprising a body with an inlet configured to receive a vapor stream, a first outlet for a superheated vapor stream and, a second outlet for a liquid stream; a baffle disposed within the body and configured to impart a swirl at or above sonic velocity to the vapor stream; an internal cavity in the body between the inlet, the first outlet, and the second outlet; and, a turbine wheel configured to transmit rotational movement from the superheated vapor stream to an electrical generator, the turbine wheel disposed between the outlet and the internal cavity.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

Une turbine avec un séparateur supersonique est disposée en amont de la turbine. Le séparateur supersonique imprime un tourbillon sur un flux de vapeur pour éliminer tout composant plus lourd. Un flux de vapeur surchauffée provenant du séparateur supersonique est passé à travers la turbine pour réduire la pression du flux de vapeur. En même temps, de l'électricité est générée par le flux de vapeur surchauffée par l'intermédiaire d'une roue de turbine. La turbine et le séparateur supersonique peuvent être formés d'un seul tenant, ou ils peuvent être des composants discrets.
PCT/US2019/022436 2018-03-16 2019-03-15 Turbine à séparation supersonique WO2019178459A1 (fr)

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Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10829698B2 (en) 2018-03-16 2020-11-10 Uop Llc Power recovery from quench and dilution vapor streams
US10871085B2 (en) 2018-03-16 2020-12-22 Uop Llc Energy-recovery turbines for gas streams
NL2022927B1 (en) * 2019-04-11 2020-10-20 Twister Bv Cyclonic fluid separator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6009711A (en) * 1997-08-14 2000-01-04 Ormat Industries Ltd. Apparatus and method for producing power using geothermal fluid
US6962199B1 (en) * 1998-12-31 2005-11-08 Shell Oil Company Method for removing condensables from a natural gas stream, at a wellhead, downstream of the wellhead choke
WO2016004014A1 (fr) * 2014-06-30 2016-01-07 Robert Kremer Appareil, système et procédé pour utiliser une énergie thermique

Family Cites Families (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4455614A (en) 1973-09-21 1984-06-19 Westinghouse Electric Corp. Gas turbine and steam turbine combined cycle electric power generating plant having a coordinated and hybridized control system and an improved factory based method for making and testing combined cycle and other power plants and control systems therefor
US4106294A (en) * 1977-02-02 1978-08-15 Julius Czaja Thermodynamic process and latent heat engine
LU80763A1 (de) 1978-01-09 1979-05-16 Lenz K Verfahren und anordnung zur steuerung,ueberwachung und verbrauchsmessung eines fluiddurchflussventiles
US4285481A (en) 1979-06-04 1981-08-25 Biscomb Lloyd I Multiple wind turbine tethered airfoil wind energy conversion system
US4292050A (en) * 1979-11-15 1981-09-29 Linhardt & Associates, Inc. Curved duct separator for removing particulate matter from a carrier gas
GR1000927B (el) * 1990-08-10 1993-03-16 Μεθοδος και μηχανισμος υπερηχητικου διαχωρισμου αεριου ροης-σταγονιδιων.
US5167123A (en) * 1992-01-13 1992-12-01 Brandon Ronald E Flow condensing diffusers for saturated vapor applications
EP0552039A1 (fr) 1992-01-17 1993-07-21 Gec-Marconi Limited Accordage d'émetteur
US5385121A (en) * 1993-01-19 1995-01-31 Keystone International Holdings Corp. Steam desuperheater
US5384489A (en) 1994-02-07 1995-01-24 Bellac; Alphonse H. Wind-powered electricity generating system including wind energy storage
US6681155B1 (en) 1998-08-31 2004-01-20 Mitsubishi Chemical Corporation Optimizing control method and optimizing control system for power plant
US6524368B2 (en) * 1998-12-31 2003-02-25 Shell Oil Company Supersonic separator apparatus and method
US6280502B1 (en) * 1998-12-31 2001-08-28 Shell Oil Company Removing solids from a fluid
US6265453B1 (en) 1999-07-01 2001-07-24 Syntroleum Corporation Hydrocarbon conversion system with enhanced combustor and method
US6261055B1 (en) * 1999-08-03 2001-07-17 Jerzy A. Owczarek Exhaust flow diffuser for a steam turbine
US6354084B1 (en) 1999-08-20 2002-03-12 Cummins Engine Company, Inc. Exhaust gas recirculation system for a turbocharged internal combustion engine
DE102009031557A1 (de) 2009-03-02 2010-09-09 Sms Siemag Ag Energierückgewinnung in Warmbandstraßen durch Umwandlung der Kühlwärme der Stranggießanlage sowie der Restwärme von Brammen und Coils in elektrische Energie oder sonstige Nutzung der aufgefangenen Prozesswärme
WO2002027892A1 (fr) * 2000-09-28 2002-04-04 Youtility Inc Reseau local de distribution d'electricite
CA2484297C (fr) 2002-04-29 2010-06-15 Marco Betting Separateur de fluide cyclonique a position de diaphragme reglable
ATE367195T1 (de) 2002-04-29 2007-08-15 Shell Int Research Überschallfluidtrennung verbessert durch einspritzung
CN1309451C (zh) 2002-09-02 2007-04-11 国际壳牌研究有限公司 旋流式流体分离器
US6898540B2 (en) 2002-11-12 2005-05-24 General Electric Company System and method for displaying real-time turbine corrected output and heat rate
US6938425B2 (en) 2003-08-11 2005-09-06 Siemens Westinghouse Power Corporation System and method for controlling water injection in a turbine engine
JP4915117B2 (ja) 2005-04-20 2012-04-11 ソニー株式会社 振動衝撃吸収機構およびコンテンツ再生装置
US7948101B2 (en) 2005-09-02 2011-05-24 John Christopher Burtch Apparatus for production of hydrogen gas using wind and wave action
US7757493B2 (en) 2006-03-07 2010-07-20 Uop Llc Fluid catalytic cracking steam pressure letdown power recovery system and process
CA2655973C (fr) 2006-06-23 2013-08-13 Saudi Arabian Oil Company Systeme, methode et produit-programme permettant de cibler et de definir la distribution optimale des elements moteurs dans les systemes de recuperation d'energie
EP1974790A1 (fr) 2007-03-26 2008-10-01 Twister B.V. Séparateur de fluide de cyclone
WO2008157503A1 (fr) 2007-06-15 2008-12-24 Shell Oil Company Systèmes et procédés de télésurveillance
US20090125152A1 (en) 2007-11-09 2009-05-14 Markron Technologies, Llc Method of measurement, control, and regulation for the solar thermal hybridization of a fossil fired rankine cycle
CA2726984C (fr) 2008-06-06 2014-12-30 Aramco Services Company Systeme, produit de programme et procedes apparentes pour le ciblage global de commodites de procede dans des conditions variables
US8398734B2 (en) 2008-08-01 2013-03-19 Twister B.V. Cyclonic separator with a volute outlet duct
RU2509272C2 (ru) 2009-02-05 2014-03-10 Твистер Б. В. Многоступенчатый циклонный сепаратор для текучей среды
WO2010117259A1 (fr) 2009-04-07 2010-10-14 Twister B.V. Systeme de separation comportant une vanne de turbulence
EP2301886A1 (fr) 2009-09-03 2011-03-30 Ammonia Casale S.A. Récupération de chaleur de déchets d'un procédé chimique et installation, en particulier pour la synthèse d'ammoniac
US8404918B2 (en) 2009-09-28 2013-03-26 Uop Llc Energy efficiency in adsorptive separation
US20110100004A1 (en) 2009-10-30 2011-05-05 Wael Faisal Al-Mazeedi Adaptive control of a concentrated solar power-enabled power plant
WO2011066823A2 (fr) 2009-12-05 2011-06-09 Jens Mehnert Procédé et dispositif permettant l'analyse de l'utilisation d'énergie lors du fonctionnement d'un système de production
DE102010001118B4 (de) * 2010-01-22 2021-05-12 Robert Bosch Gmbh Verfahren zum Betreiben einer Brennkraftmaschine mit einer Dampfkraftanlage
US8967590B2 (en) 2010-03-02 2015-03-03 Westlock Controls Corporation Micro-power generator for valve control applications
WO2011153146A1 (fr) * 2010-06-01 2011-12-08 Shell Oil Company Séparation de gaz produits par combustion
US10184229B2 (en) * 2010-07-30 2019-01-22 Robert Kremer Apparatus, system and method for utilizing thermal energy
FR2966814B1 (fr) 2010-10-28 2016-01-01 IFP Energies Nouvelles Procede de production d'hydrogene par vaporeformage d'une coupe petroliere avec production de vapeur optimisee.
US20120227440A1 (en) 2011-03-10 2012-09-13 Alstom Technology Ltd. System And Process For The Physical Absorption of Carbon Dioxide From a Flue Gas Stream
US9222410B2 (en) 2011-04-13 2015-12-29 General Electric Company Power plant
CA2780451A1 (fr) 2011-06-21 2012-12-21 Genalta Power, Inc. Generation d'energie a vitesse variable a partir de sources d'energie provenant de fluides industriels
US9085499B2 (en) 2011-11-09 2015-07-21 Uop Llc Energy efficiency in adsorptive separation
EP2620703A1 (fr) * 2012-01-25 2013-07-31 Siemens Aktiengesellschaft Dispositif d'injection d'eau pour un système de dérivation de vapeur d'une centrale électrique
US8997490B2 (en) 2012-02-02 2015-04-07 Electratherm, Inc. Heat utilization in ORC systems
GB2499991A (en) 2012-03-05 2013-09-11 Solaredge Technologies Ltd DC link circuit for photovoltaic array
JP5984687B2 (ja) * 2013-01-17 2016-09-06 三菱日立パワーシステムズ株式会社 湿分分離加熱器、及びこれを備える湿分分離加熱設備
JP2016056808A (ja) 2013-01-29 2016-04-21 日立建機株式会社 作業機械の圧油エネルギ回収装置
JP6010489B2 (ja) 2013-03-12 2016-10-19 三菱日立パワーシステムズ株式会社 熱電可変型コジェネレーションシステム
US8763625B1 (en) 2013-04-12 2014-07-01 John T. Carter Siphon pump technology and apparatuses
JP5790952B2 (ja) 2013-04-23 2015-10-07 横河電機株式会社 生産エネルギー管理システムおよびコンピュータプログラム
WO2014178079A2 (fr) 2013-04-26 2014-11-06 Eesavyasa Technologies Pvt. Ltd Systèmes d'éclairage à del utilisant une production d'énergie à base d'air comprimé, et leur procédé
CN104463341B (zh) 2013-09-25 2017-10-27 北京宜能高科科技有限公司 图表化的蒸汽动力系统分析优化方法和装置
US9764272B2 (en) 2013-10-28 2017-09-19 Energy Recovery, Inc. Systems and methods for utilizing turbine systems within gas processing systems
JP6248124B2 (ja) 2013-11-27 2017-12-13 株式会社日立製作所 再生可能エネルギー対応ガスタービンおよびその制御方法
RU2570131C2 (ru) 2014-04-09 2015-12-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") Способ работы тепловой электрической станции
WO2015175610A1 (fr) * 2014-05-13 2015-11-19 Holtec International Système de conditionnement de vapeur
US20160141878A1 (en) 2014-11-05 2016-05-19 John Anton Johansen Dc appliance system
US10088507B2 (en) 2014-12-03 2018-10-02 Saudi Arabian Oil Company Energy performance metric in hydrocarbon-producing facilities
US11060032B2 (en) 2015-01-02 2021-07-13 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
ES2947567T3 (es) 2015-05-06 2023-08-11 Vestas Wind Sys As Sistema de generación de energía de aerogenerador
JP6518526B2 (ja) * 2015-06-18 2019-05-22 三菱日立パワーシステムズ株式会社 軸流タービン
US9803930B2 (en) 2015-08-24 2017-10-31 Saudi Arabian Oil Company Power generation from waste heat in integrated hydrocracking and diesel hydrotreating facilities
US11107169B2 (en) * 2015-11-18 2021-08-31 General Electric Company Systems and methods for controlling and monitoring power assets
CN206538206U (zh) 2016-11-29 2017-10-03 江苏悦达家纺有限公司 一种可优化水质的热回收装置

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6009711A (en) * 1997-08-14 2000-01-04 Ormat Industries Ltd. Apparatus and method for producing power using geothermal fluid
US6962199B1 (en) * 1998-12-31 2005-11-08 Shell Oil Company Method for removing condensables from a natural gas stream, at a wellhead, downstream of the wellhead choke
WO2016004014A1 (fr) * 2014-06-30 2016-01-07 Robert Kremer Appareil, système et procédé pour utiliser une énergie thermique

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3765171A4 *

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JP2021516613A (ja) 2021-07-08
US20190284960A1 (en) 2019-09-19
JP7110376B2 (ja) 2022-08-01
EP3765171B1 (fr) 2024-01-17
EP3765171A4 (fr) 2022-01-05
US10794225B2 (en) 2020-10-06

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